Mixture of 2-Propanol + Benzene, 1,3-dimethyl-

2-Propanol

Name
2-Propanol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.10
CAS
67-63-0

Benzene, 1,3-dimethyl-

Name
Benzene, 1,3-dimethyl-
InChI
InChI=1S/C8H10/c1-7-4-3-5-8(2)6-7/h3-6H,1-2H3
InChI Key
IVSZLXZYQVIEFR-UHFFFAOYSA-N
Formula
C8H10
SMILES
Cc1cccc(C)c1
Mol. Weight (g/mol)
106.17
CAS
108-38-3
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Datasets

  1. γ - Surface tension liquid-gas, N/m (2)
  2. Vapor Liquid Equilibrium at Constant Pressure (2)
  3. Vapor Liquid Equilibrium at Constant Temperature (4)
  4. Excess molar volume, m3/mol (2)

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of 2-Propanol (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0000 0.0284
0.1019 0.0272
0.1933 0.0262
0.2999 0.0254
0.4024 0.0248
0.4983 0.0242
0.5957 0.0236
0.7013 0.0229
0.7952 0.0223
0.8987 0.0216
1.0000 0.0209

Surface tension liquid-gas, N/m [ref]

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of 2-Propanol (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.0000 0.0284
0.1019 0.0272
0.1933 0.0262
0.2999 0.0254
0.4024 0.0248
0.4983 0.0242
0.5957 0.0236
0.7013 0.0229
0.7952 0.0223
0.8987 0.0216
1.0000 0.0209

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of 2-Propanol (1) - Liquid y1[mol/mol] of 2-Propanol (1) - Vapour
412.25 0.0000 0.0000
403.35 0.0060 0.2210
398.85 0.0240 0.3270
386.15 0.0530 0.5400
381.55 0.0740 0.6270
367.05 0.2170 0.8030
363.35 0.3180 0.8400
362.05 0.3800 0.8540
360.25 0.5000 0.8720
359.75 0.5540 0.8900
357.85 0.7270 0.9000
357.65 0.7650 0.9200
356.65 0.8950 0.9450

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed Measured
T [K] - VLE x1[mol/mol] of 2-Propanol (1) - Liquid y1[mol/mol] of 2-Propanol (1) - Vapour
412.25 0.0000 0.0000
403.35 0.0060 0.2210
398.85 0.0240 0.3270
386.15 0.0530 0.5400
381.55 0.0740 0.6270
367.05 0.2170 0.8030
363.35 0.3180 0.8400
362.05 0.3800 0.8540
360.25 0.5000 0.8720
359.75 0.5540 0.8900
357.85 0.7270 0.9000
357.65 0.7650 0.9200
356.65 0.8950 0.9450

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 298.15 (VLE)

P [kPa] - VLE x1[mol/mol] of 2-Propanol (1) - Liquid
1.064 0.0000
3.88 0.0431
4.601 0.0892
4.952 0.1362
5.176 0.1842
5.322 0.2505
5.5 0.3333
5.642 0.4112
5.801 0.4922
5.925 0.5784
6.026 0.6745
6.085 0.7814
6.07 0.8821
5.912 0.9802
5.868 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 308.15 (VLE)

P [kPa] - VLE x1[mol/mol] of 2-Propanol (1) - Liquid
1.868 0.0000
6.47 0.0521
8.325 0.1252
9.134 0.1841
9.389 0.2372
9.673 0.3011
10.009 0.3852
10.322 0.4581
10.575 0.5292
10.818 0.5922
11.072 0.6713
11.23 0.7433
11.284 0.8214
11.072 0.9253
10.518 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 298.15 (VLE)

P [kPa] - VLE x1[mol/mol] of 2-Propanol (1) - Liquid
1.064 0.0000
3.88 0.0431
4.601 0.0892
4.952 0.1362
5.176 0.1842
5.322 0.2505
5.5 0.3333
5.642 0.4112
5.801 0.4922
5.925 0.5784
6.026 0.6745
6.085 0.7814
6.07 0.8821
5.912 0.9802
5.868 1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 308.15 (VLE)

P [kPa] - VLE x1[mol/mol] of 2-Propanol (1) - Liquid
1.868 0.0000
6.47 0.0521
8.325 0.1252
9.134 0.1841
9.389 0.2372
9.673 0.3011
10.009 0.3852
10.322 0.4581
10.575 0.5292
10.818 0.5922
11.072 0.6713
11.23 0.7433
11.284 0.8214
11.072 0.9253
10.518 1.0000

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of 2-Propanol (1) - Liquid Excess molar volume, m3/mol - Liquid
0.0304 5.7000e-08
0.0535 1.0500e-07
0.1053 1.6600e-07
0.1610 2.0000e-07
0.2191 2.2900e-07
0.2512 2.4100e-07
0.3067 2.4800e-07
0.3530 2.4700e-07
0.3990 2.3900e-07
0.4437 2.3200e-07
0.4990 2.1800e-07
0.5490 1.9800e-07
0.6011 1.7600e-07
0.6492 1.5100e-07
0.6990 1.2600e-07
0.7446 1.0000e-07
0.7977 6.9000e-08
0.8475 4.9000e-08
0.9044 2.2000e-08
0.9500 1.0000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of 2-Propanol (1) - Liquid Excess molar volume, m3/mol - Liquid
0.0304 5.7000e-08
0.0535 1.0500e-07
0.1053 1.6600e-07
0.1610 2.0000e-07
0.2191 2.2900e-07
0.2512 2.4100e-07
0.3067 2.4800e-07
0.3530 2.4700e-07
0.3990 2.3900e-07
0.4437 2.3200e-07
0.4990 2.1800e-07
0.5490 1.9800e-07
0.6011 1.7600e-07
0.6492 1.5100e-07
0.6990 1.2600e-07
0.7446 1.0000e-07
0.7977 6.9000e-08
0.8475 4.9000e-08
0.9044 2.2000e-08
0.9500 1.0000e-08

Sources

Note: These property values are available through the Cheméo API. A free account gives you an access key.